CN110631871B - Sealed piston type supercharged boiler ash taking device and method - Google Patents
Sealed piston type supercharged boiler ash taking device and method Download PDFInfo
- Publication number
- CN110631871B CN110631871B CN201910952361.9A CN201910952361A CN110631871B CN 110631871 B CN110631871 B CN 110631871B CN 201910952361 A CN201910952361 A CN 201910952361A CN 110631871 B CN110631871 B CN 110631871B
- Authority
- CN
- China
- Prior art keywords
- ash
- flue gas
- flue
- pressure
- gas outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000000034 method Methods 0.000 title claims abstract description 23
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 53
- 239000003546 flue gas Substances 0.000 claims abstract description 53
- 238000007789 sealing Methods 0.000 claims abstract description 40
- 239000011261 inert gas Substances 0.000 claims abstract description 8
- 239000002956 ash Substances 0.000 claims description 70
- 239000010881 fly ash Substances 0.000 claims description 22
- 238000005070 sampling Methods 0.000 claims description 7
- 230000005540 biological transmission Effects 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 230000008569 process Effects 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 238000000605 extraction Methods 0.000 description 7
- 238000002485 combustion reaction Methods 0.000 description 5
- 239000003245 coal Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000002309 gasification Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 244000181980 Fraxinus excelsior Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N1/00—Sampling; Preparing specimens for investigation
- G01N1/02—Devices for withdrawing samples
- G01N1/22—Devices for withdrawing samples in the gaseous state
- G01N1/2247—Sampling from a flowing stream of gas
- G01N1/2258—Sampling from a flowing stream of gas in a stack or chimney
Landscapes
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biomedical Technology (AREA)
- Molecular Biology (AREA)
- Physics & Mathematics (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Sampling And Sample Adjustment (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种取灰装置及方法,尤其涉及一种密封活塞式增压锅炉取灰装置及方法,属于锅炉取灰装置领域。The invention relates to an ash removal device and method, in particular to an ash removal device and method for a sealed piston type pressurized boiler, belonging to the field of boiler ash removal devices.
背景技术Background technique
一次能源以煤炭为主的基本格局在短期内难以改变,煤炭的清洁高效利用依然是能源转型发展的重要技术课题。火力发电厂中,飞灰是锅炉尾部烟气的重要组成部分。其物理化学分析结果对电厂运行调控、成本控制、设计改造及环境保护都具有重大意义。增压燃烧具有增加煤颗粒燃烧速率、提高燃烧效率,减少NO污染物排放量等优点。整体煤气化联合循环和加压富氧燃烧技术均涉及加压气化/燃烧过程。The basic pattern of coal-based primary energy is difficult to change in the short term, and the clean and efficient utilization of coal is still an important technical issue for energy transformation and development. In thermal power plants, fly ash is an important part of boiler tail flue gas. The results of physical and chemical analysis are of great significance for power plant operation regulation, cost control, design transformation and environmental protection. The supercharged combustion has the advantages of increasing the combustion rate of coal particles, improving the combustion efficiency, and reducing the emission of NO pollutants. Both integrated gasification combined cycle and pressurized oxy-combustion technologies involve a pressurized gasification/combustion process.
虽然增加反应压力有诸多优点,但加压条件增加了取灰难度,对取灰装置提出了更高要求。取灰过程中,由于取灰点内外侧存在巨大压差,灰样往往会随着高压烟气喷涌而出,不仅减少了取灰量、降低了取灰效率,还对环境造成污染。目前大部分的取灰装置均适用于常压锅炉,不适用于在加压条件下进行取灰。更为重要的是,这些装置在取灰过程中均会对烟道内部压力造成的巨大影响,从而破坏烟道内部烟气流动结构。除此之外,部分取灰装置均用于处理连续排灰且灰量较多的情况,其系统结构复杂、制造工艺难度大且成本高,并且无法在短时间内方便快捷地完成灰样收集工作。Although increasing the reaction pressure has many advantages, the pressurized conditions increase the difficulty of ash extraction, which puts forward higher requirements for the ash extraction device. In the process of ash removal, due to the huge pressure difference between the inside and outside of the ash point, the ash sample often spews out with the high-pressure flue gas, which not only reduces the amount of ash and the efficiency of ash removal, but also causes pollution to the environment. Most of the current ash removal devices are suitable for atmospheric pressure boilers, and are not suitable for ash removal under pressurized conditions. More importantly, these devices will have a huge impact on the internal pressure of the flue during the ash removal process, thereby destroying the flow structure of the flue gas inside the flue. In addition, some ash removal devices are used to deal with continuous ash discharge and a large amount of ash. The system structure is complex, the manufacturing process is difficult and the cost is high, and the collection of ash samples cannot be conveniently and quickly completed in a short time. Work.
发明内容SUMMARY OF THE INVENTION
发明目的:本发明提供一种在高压烟道中安全、高效、环保取灰的装置及方法,以解决上述问题。Purpose of the invention: The present invention provides a safe, efficient and environmentally friendly ash removal device and method in a high-pressure flue to solve the above problems.
技术方案:本发明的密封活塞式增压锅炉取灰装置,包括压力容器,所述压力容器上端设有入口管路,一侧设有充气阀,另一侧设有烟气出口管路,下端设有灰分出口管路,内部设有密封活塞;所述密封活塞通过调节活塞控制件上下移动,用于隔离收集到的飞灰。Technical scheme: The ash removal device of the sealed piston-type pressurized boiler of the present invention includes a pressure vessel, the upper end of the pressure vessel is provided with an inlet pipeline, one side is provided with an inflation valve, the other side is provided with a flue gas outlet pipeline, and the lower end is provided with an inlet pipeline. There is an ash outlet pipeline, and a sealing piston is arranged inside; the sealing piston is moved up and down by adjusting the piston control part to isolate the collected fly ash.
优选的,压力容器分为多段,每段可采用法兰连接。Preferably, the pressure vessel is divided into multiple sections, and each section can be connected by flanges.
所述密封活塞下降至末端时,其周侧与压力容器内壁密封贴合。When the sealing piston descends to the end, its peripheral side is in sealing contact with the inner wall of the pressure vessel.
所述密封活塞为平台形、圆锥形或圆台形。The sealing piston is in the shape of a platform, a cone or a truncated cone.
所述入口管路上设有进样阀。The inlet pipeline is provided with a sampling valve.
所述烟气出口管路上设有引风机与烟气出口阀。The flue gas outlet pipeline is provided with an induced draft fan and a flue gas outlet valve.
所述灰分出口管路上设有排灰阀。The ash outlet pipeline is provided with an ash discharge valve.
所述排灰阀前部设有转子,转子连接变速器与电机。优选的,该转子可为星型转子。The front part of the ash discharge valve is provided with a rotor, and the rotor is connected with the transmission and the motor. Preferably, the rotor can be a star rotor.
所述烟道与压力容器之间设有压差计。A differential pressure gauge is arranged between the flue and the pressure vessel.
一种密封活塞式增压锅炉取灰装置的取灰方法,包括如下步骤:An ash removal method for an ash removal device of a sealed piston-type pressurized boiler, comprising the following steps:
a、关闭所有阀门,将装置入口管路连接至烟道取样口,连接烟气出口管路至烟道出样口;a. Close all valves, connect the inlet pipeline of the device to the flue sampling port, and connect the flue gas outlet pipeline to the flue sampling port;
b、打开充气阀,向压力容器内充入惰性气体直至容器内与烟道压力相同;b. Open the inflation valve, and fill the pressure container with inert gas until the pressure in the container is the same as that of the flue;
c、关闭充气阀,打开入口管道、烟气出口管路上的阀门,携带飞灰的烟气进入压力容器,并经由烟气出口管路回到烟道,此时密封活塞与壁面分离;c. Close the inflation valve, open the valves on the inlet pipe and the flue gas outlet pipe, and the flue gas carrying the fly ash enters the pressure vessel and returns to the flue through the flue gas outlet pipe. At this time, the sealing piston is separated from the wall surface;
d、采集完毕后,关闭入口管道、烟气出口管路上的阀门,通过活塞控制件使密封活塞下移直至其与压力容器的壁面紧密贴合;d. After the collection is completed, close the valves on the inlet pipe and the flue gas outlet pipe, and move the sealing piston down through the piston control member until it is in close contact with the wall of the pressure vessel;
e、打开灰分出口管路上的阀门,将沉积的飞灰排出。e. Open the valve on the ash outlet pipeline to discharge the deposited fly ash.
所述步骤e之前还可实施以下步骤:The following steps can also be implemented before the step e:
f、打开烟气出口管路上的阀门,将密封活塞上侧空间内的高压烟气排出压力容器。f. Open the valve on the flue gas outlet pipeline, and discharge the high-pressure flue gas in the space on the upper side of the sealing piston out of the pressure vessel.
g、当烟道与压力容器的压差稳定后,关闭烟气出口管路上的阀门并上移密封活塞,使得密封活塞下侧的高压气体再次进入上侧常压空间。该步骤用于释放活塞下部残留的高压烟气。g. When the pressure difference between the flue and the pressure vessel is stable, close the valve on the flue gas outlet pipeline and move the sealing piston upward, so that the high-pressure gas on the lower side of the sealing piston enters the upper normal pressure space again. This step is used to release the high pressure flue gas remaining in the lower part of the piston.
所述取灰装置烟气出口管路设有引风机时,实施步骤b的同时关闭引风机,在实施步骤c的同时开启引风机。When the flue gas outlet pipeline of the ash extraction device is provided with an induced draft fan, the induced draft fan is turned off while performing step b, and the induced induced draft fan is turned on while performing step c.
有益效果:与现有技术相比,本发明具有如下显著优点:Beneficial effects: Compared with the prior art, the present invention has the following significant advantages:
(1)本发明方便、快捷、可靠得实现了飞灰与烟气的分离及烟气泄压工作,有效防止了普通取灰装置由于取灰内外侧压差过大造成的飞灰四溅、集灰量减少等问题。(1) The present invention is convenient, fast and reliable to realize the separation of fly ash and flue gas and the work of flue gas pressure relief, and effectively prevent the fly ash from splashing around due to the excessive pressure difference between the inner and outer sides of the ash extraction device of the common ash extraction device. The problem of reducing the amount of ash collected.
(2)本发明可在不改变高压烟道内部流动结构的同时完成取灰过程。同时,抽取的烟气均再次返回烟道,避免了烟气泄漏造成的环境污染问题。(2) The present invention can complete the ash removal process without changing the internal flow structure of the high-pressure flue. At the same time, the extracted flue gas is returned to the flue again, which avoids the problem of environmental pollution caused by flue gas leakage.
(3)本发明通过在取灰过程中充、放惰性气体,可有效减少压力容器内的飞灰残留,提高飞灰收集率。(3) The present invention can effectively reduce the residual fly ash in the pressure vessel and improve the collection rate of fly ash by charging and discharging the inert gas during the ash extraction process.
(4)本发明设置的转子,通过外接电机及变速器,可实现对飞灰排放速率的控制。同时,转子本身具有良好的密封性,可防止意外情况下压差失衡时造成的飞灰外泄问题。(4) The rotor provided in the present invention can control the discharge rate of fly ash by connecting an external motor and a transmission. At the same time, the rotor itself has good sealing, which can prevent the leakage of fly ash caused by unbalanced pressure difference under unexpected circumstances.
(5)本发明压力容器的分段式设计可有效简化拆卸组装过程,方便对其内部组件进行检查维修。尤其在锅炉燃烧高灰高硫的劣质煤种时,大量的飞灰容易对取灰装置内部部件造成一定损害,此时方便快捷的拆装设计尤为重要。(5) The segmented design of the pressure vessel of the present invention can effectively simplify the disassembly and assembly process, and facilitate the inspection and maintenance of its internal components. Especially when the boiler burns low-quality coal with high ash and high sulfur, a large amount of fly ash is likely to cause certain damage to the internal components of the ash removal device. At this time, the convenient and quick disassembly and assembly design is particularly important.
附图说明Description of drawings
图1为本发明的结构示意图;Fig. 1 is the structural representation of the present invention;
图2(a)为本发明密封活塞与容器壁面分离状态示意图;Figure 2 (a) is a schematic diagram of the separation state of the sealing piston and the container wall of the present invention;
图2(b)为本发明密封活塞与容器壁面密封状态示意图;Figure 2 (b) is a schematic diagram of the sealing state of the sealing piston of the present invention and the wall surface of the container;
图3为不同形状密封活塞结构图。Figure 3 is a structural diagram of sealing pistons with different shapes.
具体实施方式Detailed ways
下面结合附图对本发明的技术方案作进一步说明。The technical solutions of the present invention will be further described below with reference to the accompanying drawings.
如图1所示,一种密封活塞式增压锅炉取灰装置,包括压力容器2、入口管道15、烟气出口管路11以及灰分出口管路11。所述压力容器2壁面设有充气阀5与排气阀6,另一侧设有烟气出口管路11,顶部设有入口管道15,底部设有灰分出口管路16,内部设有密封活塞3。该压力容器2可分为多段,每段通过法兰连接,方便对装置内部进行检修。所述入口管路上设有进样阀13。所述烟气出口管路上设有引风机12与烟气出口阀13。所述灰分出口管路的上设有排灰阀10。所述烟道与压力容器2之间设有压差计14。As shown in FIG. 1 , an ash removal device for a sealed piston-type booster boiler includes a
所述密封活塞3可通过调节活塞控制件4上下移动,用于隔离收集到的飞灰。根据所取灰样的粘结性,密封活塞3可采用不同形状,该密封活塞可以为平台型,也可以为圆锥形或圆台型,如图3所示。平台型活塞结构最简单、质量最轻,但灰样也最易沉积在表面;圆锥型活塞结构、复杂质量大,但积灰最少;圆台型活塞则介于二者之间。The
如图2(a)所示,当密封活塞3与压力容器3壁面分离时,活塞下部空间与上部空间联通,灰分在重力的作用下在压力容器2内下落至下部空间。所述密封活塞下落至末端时,将压力容器分为隔绝的两个空间,灰分被压在压力容器3下部与灰分出口管路11中,如图2(b)所示。所述密封活塞3外侧可设有耐高温密封橡胶圈。As shown in Figure 2(a), when the
所述排灰阀上部设有转子9,连接变速器8与电机7,在变速器8及电机7的作用下调节自身转速从而控制排灰速率。转子可对飞灰起阻隔作用,对特殊情况下取灰装置内外压力失衡造成的飞灰外泄问题起到了防护作用。所述转子9外侧与压力容器壁面间空隙小于1mm,该转子9还可为星型转子,星型转子具有良好的密封性能。The upper part of the ash discharge valve is provided with a
实施例1Example 1
以实施例1对本发明的取灰方法进行详细描述,包括如下步骤:The ash extraction method of the present invention is described in detail with
a、关闭所有阀门(进样阀1、充气阀5、排气阀6、排灰阀10以及烟气出口阀13),将装置入口管路15连接至烟道取样口A,连接烟气出口管路11至烟道出样口B。a. Close all valves (
b、打开充气阀5,通过充气阀5向压力容器2内充入惰性气体,直至压力容器2内压力与烟道压力相同,此时压差计14示数为0。该惰性气体还可具有一定压力。取灰装置与烟道压力相同,在取灰过程中不会影响烟道内部的流场分布。b. Open the charging
c、关闭充气阀5,打开入口管道15、烟气出口管路11上的阀门(进样阀1、烟气出口阀13)与引风机12,携带飞灰的烟气进入压力容器2,并经由烟气出口管路11回到烟道,此时充气阀5,排气阀6,排灰阀10均处于关闭状态,且密封活塞3与压力容器2的壁面分离。c. Close the
d、一定时间后,待压力容器2及烟气出口管路11内的惰性气体全部变为烟气,关闭入口管道、烟气出口管路11上的阀门(进样阀1、烟气出口阀13)与引风机12,通过活塞控制件4使密封活塞3下移直至其与压力容器的壁面紧密贴合,由于重力的作用,绝大多数的飞灰沉积在密封活塞下侧空间内。d. After a certain period of time, when all the inert gases in the
e、打开烟气出口管路11上的烟气出口阀13与引风机12,将密封活塞3上侧空间内的高压烟气排出压力容器。e. Open the flue
f、当烟道与压力容器的压差稳定后,关闭烟气出口管路11上的上的烟气出口阀13与引风机12,并上移密封活塞3,使得之前密封活塞下侧的高压气体再次进入上侧常压空间,由于上部空间体积远远大于下部空间体积,进行一到两次泄压过程后,压力容器内部即可变为常压,且飞灰依然保留在容器内部而不被气体带出。f. When the pressure difference between the flue and the pressure vessel is stable, close the upper flue
g、打开灰分出口管路16上的阀门,并通过变速器8及电机7调节转子9转速将沉积的飞灰排出。在取灰完成后,当压力容器2内有飞灰残留时,开启充气阀5、排气阀6以及排灰阀10(其他阀门关闭),可通过充气阀5向压力容器2内通入加压惰性气体对其进行吹扫,并重复上述过程使得残留飞灰经由转子9及排灰阀10排出。g. Open the valve on the
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910952361.9A CN110631871B (en) | 2019-10-09 | 2019-10-09 | Sealed piston type supercharged boiler ash taking device and method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910952361.9A CN110631871B (en) | 2019-10-09 | 2019-10-09 | Sealed piston type supercharged boiler ash taking device and method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN110631871A CN110631871A (en) | 2019-12-31 |
CN110631871B true CN110631871B (en) | 2022-04-12 |
Family
ID=68975992
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910952361.9A Active CN110631871B (en) | 2019-10-09 | 2019-10-09 | Sealed piston type supercharged boiler ash taking device and method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110631871B (en) |
Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3583059B2 (en) * | 2000-06-29 | 2004-10-27 | 株式会社日立製作所 | Exhaust gas introduction device |
CN2720425Y (en) * | 2004-07-27 | 2005-08-24 | 杨上雄 | Fly ash sampling device |
CN2840002Y (en) * | 2005-09-16 | 2006-11-22 | 郑忠信 | Non-power cyclone separating fly ash sampler mounted on flue |
CN101241033A (en) * | 2008-03-14 | 2008-08-13 | 东南大学 | Anti-clogging pressure taking pipe of dense gas-solid flow device and its application method |
CN202013289U (en) * | 2011-03-09 | 2011-10-19 | 东北电力科学研究院有限公司 | Anti-clogging type constant velocity fly ash sampler |
CN102749225A (en) * | 2012-07-11 | 2012-10-24 | 广东电网公司电力科学研究院 | Constant-speed continuous pulverized coal sampling device |
CN203719956U (en) * | 2013-12-18 | 2014-07-16 | 天津鹰麟节能科技发展有限公司 | Sealed flying-ash sampling device |
CN203849060U (en) * | 2014-05-17 | 2014-09-24 | 国家电网公司 | Fixed fly ash sampler capable of regulating fly ash quantity |
CN204630782U (en) * | 2015-06-02 | 2015-09-09 | 华电国际电力股份有限公司技术服务中心 | A kind of fume duct fly ash sampler |
CN106501031A (en) * | 2016-12-01 | 2017-03-15 | 南京弗诺特测控科技有限公司 | A kind of fly ash constant speed sampling is quantitative to receive grey automatic carbon testing device |
CN206573338U (en) * | 2017-01-10 | 2017-10-20 | 万达集团股份有限公司 | A kind of fly ash sampling device |
CN207081589U (en) * | 2017-06-14 | 2018-03-09 | 中国大唐集团科学技术研究院有限公司华中分公司 | A kind of fly ash sampling device |
CN207280819U (en) * | 2017-10-10 | 2018-04-27 | 江苏加怡热电有限公司 | A kind of fly ash sampler |
CN110031266A (en) * | 2018-01-11 | 2019-07-19 | 四川天法科技有限公司 | A kind of spiral-flow type flue gas Fly ash sampling pipe |
US10378416B2 (en) * | 2015-05-29 | 2019-08-13 | Fuji Electric Co., Ltd. | Analyzing apparatus and exhaust gas treating system |
-
2019
- 2019-10-09 CN CN201910952361.9A patent/CN110631871B/en active Active
Patent Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3583059B2 (en) * | 2000-06-29 | 2004-10-27 | 株式会社日立製作所 | Exhaust gas introduction device |
CN2720425Y (en) * | 2004-07-27 | 2005-08-24 | 杨上雄 | Fly ash sampling device |
CN2840002Y (en) * | 2005-09-16 | 2006-11-22 | 郑忠信 | Non-power cyclone separating fly ash sampler mounted on flue |
CN101241033A (en) * | 2008-03-14 | 2008-08-13 | 东南大学 | Anti-clogging pressure taking pipe of dense gas-solid flow device and its application method |
CN202013289U (en) * | 2011-03-09 | 2011-10-19 | 东北电力科学研究院有限公司 | Anti-clogging type constant velocity fly ash sampler |
CN102749225A (en) * | 2012-07-11 | 2012-10-24 | 广东电网公司电力科学研究院 | Constant-speed continuous pulverized coal sampling device |
CN203719956U (en) * | 2013-12-18 | 2014-07-16 | 天津鹰麟节能科技发展有限公司 | Sealed flying-ash sampling device |
CN203849060U (en) * | 2014-05-17 | 2014-09-24 | 国家电网公司 | Fixed fly ash sampler capable of regulating fly ash quantity |
US10378416B2 (en) * | 2015-05-29 | 2019-08-13 | Fuji Electric Co., Ltd. | Analyzing apparatus and exhaust gas treating system |
CN204630782U (en) * | 2015-06-02 | 2015-09-09 | 华电国际电力股份有限公司技术服务中心 | A kind of fume duct fly ash sampler |
CN106501031A (en) * | 2016-12-01 | 2017-03-15 | 南京弗诺特测控科技有限公司 | A kind of fly ash constant speed sampling is quantitative to receive grey automatic carbon testing device |
CN206573338U (en) * | 2017-01-10 | 2017-10-20 | 万达集团股份有限公司 | A kind of fly ash sampling device |
CN207081589U (en) * | 2017-06-14 | 2018-03-09 | 中国大唐集团科学技术研究院有限公司华中分公司 | A kind of fly ash sampling device |
CN207280819U (en) * | 2017-10-10 | 2018-04-27 | 江苏加怡热电有限公司 | A kind of fly ash sampler |
CN110031266A (en) * | 2018-01-11 | 2019-07-19 | 四川天法科技有限公司 | A kind of spiral-flow type flue gas Fly ash sampling pipe |
Non-Patent Citations (1)
Title |
---|
火力发电厂飞灰取样装置性能分析与改进;刘景龙;《山东电力技术》;20161231;51-55 * |
Also Published As
Publication number | Publication date |
---|---|
CN110631871A (en) | 2019-12-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202417889U (en) | Natural gas compressor and recovery system | |
CN104023818A (en) | Systems for capturing polluting emissions | |
CN110631871B (en) | Sealed piston type supercharged boiler ash taking device and method | |
CN103451378B (en) | The vacuum pipe automatic ash removing system and method for liquid steel refining dry-type vacuum pumping system | |
CN210140604U (en) | Recovery device for blast furnace damping-down and diffusing coal gas | |
CN204723967U (en) | Purification of air dedusting blowdown cleaning device | |
CN204709989U (en) | Saving low pulse dust collector | |
CN206817489U (en) | One kind supercharging fume extractor | |
CN203228116U (en) | Grinding machining dust removal device | |
CN107339220B (en) | Dual reflux oil separates taper orifice plate noise reduction compressor periodic off-gases recyclable device | |
CN202882857U (en) | Self-controlled oil well casing gas recovery device | |
CN202052444U (en) | Material absorption dust removing device for filling materials of carbon roaster | |
CN209816032U (en) | A kind of alkane gas preparation, desulfurization and detarring device | |
CN205235671U (en) | Oil -gas separator | |
CN203006484U (en) | Bulk cargo conveying system for ocean workboat | |
CN201331080Y (en) | Bowl-type coal grinding mill stone coal processing recycling device | |
CN206793396U (en) | Closed circulation deaerating plant | |
CN206184189U (en) | Electric automated dust removal device | |
CN202087433U (en) | A cyclone dust collector used for dust removal of phthalic anhydride chip packaging | |
CN201415094Y (en) | A gas-liquid separation device used in the waste tire system | |
CN1254806A (en) | High-speed full-pressure exhaustion valve | |
CN219355715U (en) | Oil fume separator | |
CN218209618U (en) | Slag discharging device for boiler | |
CN203940452U (en) | A kind of water spray smoke-eliminating chimney system | |
CN201661339U (en) | Gas-oil separation device of engine crank case |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |